Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -1912.50 ± 0.42 | kJ/mol | NIST |
ΔfG° | -116.47 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -190.20 ± 0.54 | kJ/mol | NIST |
ΔfH°liquid | -233.10 ± 0.46 | kJ/mol | NIST |
ΔfusH° | 7.41 | kJ/mol | Joback Calculated Property |
ΔvapH° | [42.90; 42.90] | kJ/mol | |
ΔvapH° | 42.90 | kJ/mol | NIST |
ΔvapH° | 42.90 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 42.90 | kJ/mol | NIST |
ΔvapH° | 42.90 ± 0.10 | kJ/mol | NIST |
IE | 9.60 ± 0.02 | eV | NIST |
log10WS | -0.60 | Crippen Calculated Property | |
logPoct/wat | 0.447 | Crippen Calculated Property | |
McVol | 59.500 | ml/mol | McGowan Calculated Property |
NFPA Fire | 2 | KDB | |
NFPA Health | 2 | KDB | |
NFPA Safety | 2 | KDB | |
Pc | 5335.72 | kPa | Joback Calculated Property |
Inp | 709.20 | NIST | |
Tboil | [399.20; 400.60] | K | |
Tboil | 400.60 | K | NIST |
Tboil | 399.20 | K | NIST |
Tboil | 400.15 | K | NIST |
Tc | 616.42 | K | Joback Calculated Property |
Tfus | 266.15 ± 2.00 | K | NIST |
Vc | 0.222 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [106.51; 144.43] | J/mol×K | [400.53; 616.42] | |
T(K) Ideal gas heat capacity (J/mol×K) 110 120 130 140 400 500 600 | ||||
Cp,gas | 106.51 | J/mol×K | 400.53 | Joback Calculated Property |
Cp,gas | 113.46 | J/mol×K | 436.51 | Joback Calculated Property |
Cp,gas | 120.16 | J/mol×K | 472.49 | Joback Calculated Property |
Cp,gas | 126.61 | J/mol×K | 508.47 | Joback Calculated Property |
Cp,gas | 132.81 | J/mol×K | 544.46 | Joback Calculated Property |
Cp,gas | 138.75 | J/mol×K | 580.44 | Joback Calculated Property |
Cp,gas | 144.43 | J/mol×K | 616.42 | Joback Calculated Property |
ΔvapH | [36.80; 42.90] | kJ/mol | [342.50; 399.20] | |
ΔvapH | 42.90 | kJ/mol | 342.50 | NIST |
ΔvapH | 36.80 | kJ/mol | 399.20 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 342.70 | K | 13.30 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [0.19; 202.67] | kPa | [266.65; 425.65] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.53129e+01 | |||
Coefficient B | -3.86501e+03 | |||
Coefficient C | -3.92000e+01 | |||
Temperature range, min. | 266.65 | |||
Temperature range, max. | 425.65 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 0.19 | kPa | 266.65 | Calculated Property |
Pvap | 0.63 | kPa | 284.32 | Calculated Property |
Pvap | 1.83 | kPa | 301.98 | Calculated Property |
Pvap | 4.62 | kPa | 319.65 | Calculated Property |
Pvap | 10.47 | kPa | 337.32 | Calculated Property |
Pvap | 21.62 | kPa | 354.98 | Calculated Property |
Pvap | 41.34 | kPa | 372.65 | Calculated Property |
Pvap | 74.08 | kPa | 390.32 | Calculated Property |
Pvap | 125.52 | kPa | 407.98 | Calculated Property |
Pvap | 202.67 | kPa | 425.65 | Calculated Property |
Pvap | [0.18; 5961.07] | kPa | [266.65; 616.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 3.76192e+01 | |||
Coefficient B | -6.01856e+03 | |||
Coefficient C | -3.00236e+00 | |||
Coefficient D | 3.40369e-07 | |||
Temperature range, min. | 266.65 | |||
Temperature range, max. | 616.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 300 400 500 600 | ||||
Pvap | 0.18 | kPa | 266.65 | Calculated Property |
Pvap | 2.16 | kPa | 305.47 | Calculated Property |
Pvap | 14.01 | kPa | 344.28 | Calculated Property |
Pvap | 60.34 | kPa | 383.10 | Calculated Property |
Pvap | 193.68 | kPa | 421.92 | Calculated Property |
Pvap | 500.43 | kPa | 460.73 | Calculated Property |
Pvap | 1096.99 | kPa | 499.55 | Calculated Property |
Pvap | 2117.59 | kPa | 538.37 | Calculated Property |
Pvap | 3698.11 | kPa | 577.18 | Calculated Property |
Pvap | 5961.07 | kPa | 616.00 | Calculated Property |
Find more compounds similar to 2-Oxetanone, 4-methylene-.
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